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Hydrothermal synthesis of unsupported MoS2 as catalyst for hydrodesulfurization of gas oil

机译:无支持MOS2的水热合成作为瓦斯油加氢硫化的催化剂

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Hydrothermal synthesis with ammonium heptamolybdate and thiourea as precursors was used to obtain an unsupported MoS2 catalyst. The catalyst was obtained in sulfide state directly at mild reaction conditions (i.e., 180 degrees C during 5h). After catalyst was obtained, it was characterized through nitrogen physisorption, transmission electron microscopy, energy-dispersive spectroscopy, X-ray diffraction, and X-ray photoelectron spectroscopy. Catalytic evaluation was carried out in a batch reactor at 350 degrees C, 55 bar of hydrogen pressure, 750rpm, and 3h of reaction time using straight-run gas oil (SRGO) as feedstock. A commercial CoMo/Al2O3 catalyst was used for comparison of activity. The synthesized catalyst was slightly more active toward SRGO hydrodesulfurization than commercial one keeping constant the sulfur removal after two runs.
机译:使用氢铵钼酸铵和硫脲作为前体的水热合成,得到不支持的MOS2催化剂。 在温和的反应条件下直接在硫化物状态下在温和的反应条件下(180℃,5h)获得催化剂。 得到催化剂后,通过氮原料,透射电子显微镜,能量分散光谱,X射线衍射和X射线光电子能谱表征。 使用直流瓦斯油(SRGO)作为原料,在350℃,55巴的氢气压力,750rpm和3h中,在350℃,55巴的氢气压力,750rpm和3h中进行催化评价。 商业COMO / AL2O3催化剂用于比较活性。 合成的催化剂略高于SRO加氢脱硫,而不是商业单保持恒定在两次运行后的硫去除。

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